CN105958098A - High-efficiency compound regenerative electrical energy device - Google Patents
High-efficiency compound regenerative electrical energy device Download PDFInfo
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- CN105958098A CN105958098A CN201610262375.4A CN201610262375A CN105958098A CN 105958098 A CN105958098 A CN 105958098A CN 201610262375 A CN201610262375 A CN 201610262375A CN 105958098 A CN105958098 A CN 105958098A
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- Prior art keywords
- pump
- reactor
- cathode chamber
- anode chamber
- chamber
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
- H01M8/184—Regeneration by electrochemical means
- H01M8/188—Regeneration by electrochemical means by recharging of redox couples containing fluids; Redox flow type batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0662—Treatment of gaseous reactants or gaseous residues, e.g. cleaning
- H01M8/0675—Removal of sulfur
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
The invention provides a high-efficiency compound regenerative electrical energy device. The device comprises a reactor, an anode chamber, an anode plate, a cathode chamber, a cathode plate, a proton exchange membrane module, a liquid distributor, a gas distributor, a purge distributor, a battery load, an output pump, a circulating pump, a heating/cooling device, a slurry pump, an air blower, a purge gas stop valve, a flow control valve, a magnetic flap liquidometer, a self-operated pressure-regulating valve, and an immersed pump. The gas distributor is disposed at the bottom of the cathode chamber, and the circulating pump is disposed in the middle of the reactor barrel. The air blower communicates with the gas distributor by the self-operated pressure-regulating valve, and the immersed pump is disposed at the bottom of the cathode chamber. The device uses the coupling mode of fuel cell and catalyst reactivation by means of the arrangement of air cathode fuel cell, is beneficial to improve the oxidation regeneration rate of the catalyst, and realizes the rapid regeneration of the complex catalyst.
Description
Technical field
The present invention relates to desulfurizing and purifying apparatus field, particularly relate to a kind of high efficiency composition regenerative electric energy device.
Background technology
Along with society's pay attention to day by day to environmental conservation, the discharge effectively controlling sulphur-containing exhaust gas has become country's ring
A part for border planning.In Industrial cleaning facility fields such as petrochemical industry, natural gas, oil field development, coke-stove gas
In, sulfur-containing gas uses in the acid gas that either physically or chemically deacidification is discharged after processing often containing H2S, need into
One step vent gas treatment, could qualified discharge.Containing H2The process of S-acid gas, generally uses Clause sulfur recovery work
Skill (deriving technique containing various improvement) and liquid phase direct oxidation process.Clause sulfur recovery technology is in acid gas
H2S concentration requirement is strict, this technological process is complicated, equipment and auxiliary facility is many, investment payback time length, occupation of land
Area is big, especially to H2The adaptability for working condition that S concentration is too low or content fluctuation is bigger is poor.Liquid phase direct oxidation
The most representational in technique have Stretfoul oxidizing process, LO-CAT technique, SulFerox technique etc., shows
Some selexol process Complexing Iron catalyst coupling regeneration coproduction electrical energy devices also exists that energy consumption is big, reaction rate
Slowly, the problem of chelating agent degraded.
Therefore, a kind of high efficiency composition regenerative electric energy device of invention seems the most necessary.
Summary of the invention
In order to solve above-mentioned technical problem, the present invention provides a kind of high efficiency composition regenerative electric energy device existing to solve
With the presence of the energy consumption of desulfurization regeneration electrical energy devices big, reaction rate slow, the problem of chelating agent degraded.A kind of
High efficiency composition regenerative electric energy device includes reactor, anode chamber, positive plate, cathode chamber, minus plate, proton
Exchange membrane assembly, liquid distribution trough, gas distributor, purge distributor, cell load, rear pump, follow
Ring pump, heating/cooling device, serosity pump, aerator, purge gas stop valve, flow control valve, magnetic turnover panel liquid
Position meter, Self-driven pressure-adjusting valve and immersed pump, described anode chamber is arranged on reactor urceolus;Described anode
Plate is arranged on the inside of anode chamber;Described cathode chamber is arranged in reactor inner core;Described minus plate sets
Putting the inwall at cathode chamber, described proton exchange membrane module is arranged between anode chamber and cathode chamber;Described
Liquid distribution trough be arranged on the top of anode chamber;Described gas distributor is arranged on the lower section of cathode chamber;
Described cell load is arranged on the top of reactor;Described rear pump is arranged at bottom reactor shell;
Described circulating pump is arranged in the middle part of reactor shell;Described serosity pump is arranged at at reactor the cone end;
Described aerator is connected with gas distributor by Self-driven pressure-adjusting valve;Described immersed pump is arranged at the moon
Bottom room, pole.
Proton exchange membrane module is specifically set between described anode chamber and cathode chamber, advantageously allows proton and exist
Move between it, in order to form redox reaction.
Between described positive plate and minus plate, concrete employing copper cash is connected, and advantageously forms closed-loop path, defeated
Go out electric energy.
Described proton exchange membrane module specifically use PEM and be arranged on outside PEM stainless
The combination of steel wire, advantageously ensures that the structural strength of PEM.
Described positive plate specifically uses carbon felt or carbon cloth material plate, is conducive to improving contact area, and raising is led
Electrical property, and have easy machine-shaping, internal resistance that the advantages such as little is lost.
The air electrode that described minus plate specifically uses platinum carbon to be catalyst does reaction electrode, the most compound
Layer structure, is followed successively by from top to bottom: outside platinum carbon Catalytic Layer, carbon based layer, diffusion layer, collection water layer, many skies
Wall clamping plate, are conducive to improving further electric conductivity, improve desulfuration efficiency.
Compared with prior art, there is advantages that the present invention passes through air cathode fuel electricity
The setting in pond, uses fuel cell and catalyst regenerative coupling mode, is conducive to improving the oxidation of catalyst again
Raw speed, it is achieved the rapid regeneration of complex catalyst, is conducive to associating battery process to produce electric energy, it is achieved energy
The secondary of amount utilizes, and advantageously reduces the energy consumption of regenerative process and the degraded loss of catalyst.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described further:
In figure:
1-reactor, 2-anode chamber, 3-positive plate, 4-cathode chamber, 5-minus plate, 6-PEM group
Part, 7-liquid distribution trough, 8-gas distributor, 9-purges distributor, 10-cell load, 11-rear pump,
12-circulating pump, 13-heating/cooling device, 14-serosity pump, 15-aerator, 16-purge gas stop valve, 17-
Flow control valve, 18-magnetic flap level gauge, 19-Self-driven pressure-adjusting valve, 20-immersed pump.
Embodiment:
As shown in Figure 1
The present invention provides a kind of high efficiency composition regenerative electric energy device, including reactor 1, anode chamber 2, positive plate
3, cathode chamber 4, minus plate 5, proton exchange membrane module 6, liquid distribution trough 7, gas distributor 8, blows
Sweep distributor 9, cell load 10, rear pump 11, circulating pump 12, heating/cooling device 13, serosity pump 14,
Aerator 15, purge gas stop valve 16, flow control valve 17, magnetic flap level gauge 18, self-operated type pressure regulation
Valve 19, immersed pump 20.Described anode chamber 2 is arranged on reactor 1 urceolus;Described positive plate 3 is arranged
Inside in anode chamber 2;Described cathode chamber 4 is arranged in reactor 1 inner core;Described minus plate 5
It is arranged on the inwall of cathode chamber 4;Described proton exchange membrane module 6 is arranged on anode chamber 2 and cathode chamber 4
Between;Described liquid distribution trough 7 is arranged on the top of anode chamber 2;Described gas distributor 8 is arranged
Lower section at cathode chamber 4;Described cell load 10 is arranged on the top of reactor 1;Described rear pump
11 are arranged at reactor 1 cylinder body bottom;Described circulating pump 12 is arranged in the middle part of reactor 1 cylinder, circulation
Pump 12 outlet is furnished with heating/cooling device 13;Described serosity pump 14 is arranged at reactor 1 and bores at the end;Institute
The aerator 15 stated is connected with gas distributor 8 by Self-driven pressure-adjusting valve 19;Described immersed pump 20
It is arranged at bottom cathode chamber 4.
Between described anode chamber 2 and cathode chamber 4, proton exchange membrane module 6 is specifically set, advantageously allows matter
Son moves in-between, in order to form redox reaction.
Between described positive plate 3 and minus plate 5, concrete employing copper cash is connected, and advantageously forms closed-loop path,
Output electric energy.
Described proton exchange membrane module 6 specifically uses PEM and is arranged on outside PEM not
The combination of rust steel wire, advantageously ensures that the structural strength of PEM.
Described positive plate 3 specifically uses carbon felt or carbon cloth material plate, is conducive to improving contact area, improves
Electric conductivity, and have easy machine-shaping, internal resistance that the advantages such as little is lost.
The air electrode that described minus plate 4 specifically uses platinum carbon to be catalyst does reaction electrode, the most multiple
Close layer structure, be followed successively by from top to bottom: be platinum carbon Catalytic Layer, carbon based layer, diffusion layer, collection water layer, how empty
Outer wall clamping plate, are conducive to improving further electric conductivity, improve desulfuration efficiency.
Operation principle
The present invention passes through the Complexing Iron catalyst rich in Fe (II) through liquid distribution trough 7, liquid distribution trough 7
For loop configuration, uniformly spray is to anode chamber 2 peripheral in regeneration reactor 1, and positive plate 3 is immersed in anode chamber
2, for ensureing that anode chamber 2 maintains certain liquid level, control output by magnetic flap level gauge 18 remote transmitting sensor
The flow control valve 17 of pump 11 outlet, fuel battery negative pole is air cathode, and minus plate 5 is embedded in cathode chamber 4
Inwall, the gas distributor 8 that air connects via aerator 15 is to cathode chamber 4 air-blowing, gas distributor 8
Using superposition radiation air-blowing mode, be passed through air is dispersed in around minus plate 5, positive plate 3 and the moon
Between pole plate 5, concrete employing copper cash is connected, to form closed-loop path.Fe (II) spontaneous oxidation in catalyst
Lose electronics e-Generate Fe (III), the electronics e lost-Through conducting medium, UNICOM's external cell load 10 biography
It is delivered to minus plate 5, with electron acceptor (O2) contact, between anode chamber 2 and cathode chamber 4, proton exchange is set
Membrane module 6, the proton H in anode chamber 2+Minus plate 5 can be delivered to by proton exchange membrane module 6
, through the catalysis of platinum carbon, there is reduction reaction, produce free of contamination water in Catalytic Layer.
Anode: Fe (II) → Fe (III)+e-;
Negative electrode: O2+4e-+4H+→2H2O;
Overall reaction: 4Fe (II)+O2+4H+→2H2O+4Fe(III)
Use fuel cell and catalyst regenerative coupling mode can be effectively improved fuel cell efficiency, thus improve
Desulfuration efficiency, it is achieved electric energy and the coproduction of catalyst regeneration.
Utilize technical solutions according to the invention, or those skilled in the art's opening in technical solution of the present invention
Give, design similar technical scheme, and reach above-mentioned technique effect, all fall into the guarantor of the present invention
Protect scope.
Claims (5)
1. a high efficiency composition regenerative electric energy device, it is characterised in that this new type natural desulfurization Complexing Iron is urged
Agent coupling regeneration coproduction electrical energy devices includes reactor (1), anode chamber (2), positive plate (3), the moon
Room, pole (4), minus plate (5), proton exchange membrane module (6), liquid distribution trough (7), gas divides
Cloth device (8), purging distributor (9), cell load (10), rear pump (11), circulating pump (12),
Heating/cooling device (13), serosity pump (14), aerator (15), purge gas stop valve (16), stream
Adjustable valve (17), magnetic flap level gauge (18), Self-driven pressure-adjusting valve (19), immersed pump (20),
Described anode chamber (2) is arranged on reactor (1) urceolus;Described positive plate (3) is arranged on anode chamber
(2) inside;Described cathode chamber (4) is arranged in reactor (1) inner core;Described minus plate (5)
It is arranged on the inwall of cathode chamber (4);Described proton exchange membrane module (6) be arranged on anode chamber (2) and
Between cathode chamber (4);Described liquid distribution trough (7) is arranged on the top of anode chamber (2);Described
Gas distributor (8) is arranged on the lower section of cathode chamber (4);Described cell load (10) is arranged on instead
Answer the top of device (1);Described rear pump (11) is arranged at reactor (1) cylinder body bottom;Described
Circulating pump (12) is arranged in the middle part of reactor (1) cylinder, and circulating pump (12) outlet is furnished with heating/cooling device
(13);Described serosity pump (14) is arranged at at reactor (1) the cone end;Described aerator (15)
It is connected with gas distributor (8) by Self-driven pressure-adjusting valve (19);Described immersed pump (20) is arranged
In cathode chamber (4) bottom.
2. new type natural desulfurization Complexing Iron catalyst coupling regeneration coproduction electric energy as claimed in claim 1
Device, it is characterised in that between described anode chamber (2) and cathode chamber (4), proton exchange is specifically set
Membrane module (6).
3. new type natural desulfurization Complexing Iron catalyst coupling regeneration coproduction electric energy as claimed in claim 1
Device, it is characterised in that between described positive plate (3) and minus plate (5), concrete employing copper cash is connected.
4. new type natural desulfurization Complexing Iron catalyst coupling regeneration coproduction electric energy dress as claimed in claim 2
Put, it is characterised in that described proton exchange membrane module (6) specifically uses PEM and is arranged on proton
The combination of the stainless steel cloth outside exchange membrane.
5. new type natural desulfurization Complexing Iron catalyst coupling regeneration coproduction electric energy as claimed in claim 1
Device, it is characterised in that described positive plate (3) specifically uses carbon felt or carbon cloth material plate.
Priority Applications (1)
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CN201610262375.4A CN105958098A (en) | 2016-04-25 | 2016-04-25 | High-efficiency compound regenerative electrical energy device |
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CN201610262375.4A CN105958098A (en) | 2016-04-25 | 2016-04-25 | High-efficiency compound regenerative electrical energy device |
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Publication Number | Publication Date |
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